RU2664543C2 - Способы и системы для получения ароматических соединений из углеводородов каталитического крекинга - Google Patents
Способы и системы для получения ароматических соединений из углеводородов каталитического крекинга Download PDFInfo
- Publication number
- RU2664543C2 RU2664543C2 RU2015116113A RU2015116113A RU2664543C2 RU 2664543 C2 RU2664543 C2 RU 2664543C2 RU 2015116113 A RU2015116113 A RU 2015116113A RU 2015116113 A RU2015116113 A RU 2015116113A RU 2664543 C2 RU2664543 C2 RU 2664543C2
- Authority
- RU
- Russia
- Prior art keywords
- stream
- aromatic compounds
- section
- xylene
- cstream
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 46
- 238000004523 catalytic cracking Methods 0.000 title claims abstract description 16
- 150000001491 aromatic compounds Chemical class 0.000 title claims description 37
- 229930195733 hydrocarbon Natural products 0.000 title abstract description 16
- 150000002430 hydrocarbons Chemical class 0.000 title abstract description 14
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims abstract description 93
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims abstract description 72
- URLKBWYHVLBVBO-UHFFFAOYSA-N Para-Xylene Chemical group CC1=CC=C(C)C=C1 URLKBWYHVLBVBO-UHFFFAOYSA-N 0.000 claims abstract description 69
- 239000008096 xylene Substances 0.000 claims abstract description 32
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims abstract description 30
- 238000000605 extraction Methods 0.000 claims abstract description 24
- 238000000926 separation method Methods 0.000 claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 claims abstract description 22
- 150000001336 alkenes Chemical class 0.000 claims abstract description 20
- 239000012535 impurity Substances 0.000 claims abstract description 14
- 238000004821 distillation Methods 0.000 claims abstract description 11
- 238000006317 isomerization reaction Methods 0.000 claims abstract description 10
- 238000001833 catalytic reforming Methods 0.000 claims abstract description 5
- 238000007233 catalytic pyrolysis Methods 0.000 claims abstract 4
- FGUUSXIOTUKUDN-IBGZPJMESA-N C1(=CC=CC=C1)N1C2=C(NC([C@H](C1)NC=1OC(=NN=1)C1=CC=CC=C1)=O)C=CC=C2 Chemical compound C1(=CC=CC=C1)N1C2=C(NC([C@H](C1)NC=1OC(=NN=1)C1=CC=CC=C1)=O)C=CC=C2 FGUUSXIOTUKUDN-IBGZPJMESA-N 0.000 claims abstract 2
- 230000015572 biosynthetic process Effects 0.000 claims description 14
- 239000003054 catalyst Substances 0.000 claims description 10
- 238000000638 solvent extraction Methods 0.000 claims description 7
- 238000000895 extractive distillation Methods 0.000 claims description 6
- 230000003197 catalytic effect Effects 0.000 claims description 5
- 238000000622 liquid--liquid extraction Methods 0.000 claims description 5
- 238000001179 sorption measurement Methods 0.000 claims description 4
- 230000020335 dealkylation Effects 0.000 claims description 3
- 238000006900 dealkylation reaction Methods 0.000 claims description 3
- 238000005984 hydrogenation reaction Methods 0.000 claims description 3
- 238000010521 absorption reaction Methods 0.000 claims description 2
- 230000008929 regeneration Effects 0.000 claims description 2
- 238000011069 regeneration method Methods 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 16
- 239000003502 gasoline Substances 0.000 description 14
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 10
- 238000010555 transalkylation reaction Methods 0.000 description 10
- 238000004231 fluid catalytic cracking Methods 0.000 description 9
- 230000011987 methylation Effects 0.000 description 9
- 238000007069 methylation reaction Methods 0.000 description 9
- 239000000047 product Substances 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 8
- 239000004215 Carbon black (E152) Substances 0.000 description 7
- 238000007323 disproportionation reaction Methods 0.000 description 7
- 238000005899 aromatization reaction Methods 0.000 description 6
- -1 polyethylene terephthalate Polymers 0.000 description 6
- 238000000197 pyrolysis Methods 0.000 description 6
- 150000003738 xylenes Chemical class 0.000 description 6
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 5
- WOZVHXUHUFLZGK-UHFFFAOYSA-N dimethyl terephthalate Chemical compound COC(=O)C1=CC=C(C(=O)OC)C=C1 WOZVHXUHUFLZGK-UHFFFAOYSA-N 0.000 description 5
- 239000003915 liquefied petroleum gas Substances 0.000 description 4
- IVSZLXZYQVIEFR-UHFFFAOYSA-N m-xylene Chemical group CC1=CC=CC(C)=C1 IVSZLXZYQVIEFR-UHFFFAOYSA-N 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- 238000005336 cracking Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 229920000139 polyethylene terephthalate Polymers 0.000 description 3
- 239000005020 polyethylene terephthalate Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000002407 reforming Methods 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 150000003464 sulfur compounds Chemical class 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- ZQRGREQWCRSUCI-UHFFFAOYSA-N [S].C=1C=CSC=1 Chemical compound [S].C=1C=CSC=1 ZQRGREQWCRSUCI-UHFFFAOYSA-N 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 239000013462 industrial intermediate Substances 0.000 description 1
- 239000004434 industrial solvent Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- LVTJOONKWUXEFR-FZRMHRINSA-N protoneodioscin Natural products O(C[C@@H](CC[C@]1(O)[C@H](C)[C@@H]2[C@]3(C)[C@H]([C@H]4[C@@H]([C@]5(C)C(=CC4)C[C@@H](O[C@@H]4[C@H](O[C@H]6[C@@H](O)[C@@H](O)[C@@H](O)[C@H](C)O6)[C@@H](O)[C@H](O[C@H]6[C@@H](O)[C@@H](O)[C@@H](O)[C@H](C)O6)[C@H](CO)O4)CC5)CC3)C[C@@H]2O1)C)[C@H]1[C@H](O)[C@H](O)[C@H](O)[C@@H](CO)O1 LVTJOONKWUXEFR-FZRMHRINSA-N 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2729—Changing the branching point of an open chain or the point of substitution on a ring
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/76—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2729—Changing the branching point of an open chain or the point of substitution on a ring
- C07C5/2732—Catalytic processes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G55/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process
- C10G55/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only
- C10G55/06—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only including at least one catalytic cracking step
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1074—Vacuum distillates
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1077—Vacuum residues
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Mechanical Engineering (AREA)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201261711934P | 2012-10-10 | 2012-10-10 | |
US61/711,934 | 2012-10-10 | ||
PCT/US2013/031146 WO2014058465A1 (en) | 2012-10-10 | 2013-03-14 | Processes and systems for obtaining aromatics from catalytic cracking hydrocarbons |
Publications (2)
Publication Number | Publication Date |
---|---|
RU2015116113A RU2015116113A (ru) | 2016-11-27 |
RU2664543C2 true RU2664543C2 (ru) | 2018-08-20 |
Family
ID=50433205
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU2015116113A RU2664543C2 (ru) | 2012-10-10 | 2013-03-14 | Способы и системы для получения ароматических соединений из углеводородов каталитического крекинга |
Country Status (18)
Country | Link |
---|---|
US (1) | US10308567B2 (de) |
EP (1) | EP2906663B1 (de) |
JP (1) | JP6119062B2 (de) |
KR (1) | KR101995233B1 (de) |
CN (1) | CN104919026B (de) |
AR (1) | AR092980A1 (de) |
AU (1) | AU2013330434A1 (de) |
BR (1) | BR112015008035A2 (de) |
CA (1) | CA2888111A1 (de) |
IL (1) | IL238173A0 (de) |
IN (1) | IN2015DN03742A (de) |
MX (1) | MX2015004456A (de) |
MY (1) | MY183432A (de) |
PL (1) | PL2906663T3 (de) |
RU (1) | RU2664543C2 (de) |
SG (1) | SG11201502727YA (de) |
TW (1) | TWI622572B (de) |
WO (1) | WO2014058465A1 (de) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2787755C1 (ru) * | 2019-02-04 | 2023-01-12 | Чайна Петролеум Энд Кемикал Корпорейшн | Способ получения фенола и ксилолов |
Families Citing this family (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101917490B1 (ko) * | 2014-06-30 | 2018-11-09 | 엑손모빌 케미칼 패턴츠 인코포레이티드 | 파라-크실렌의 제조 방법 |
KR101917491B1 (ko) * | 2014-06-30 | 2018-11-09 | 엑손모빌 케미칼 패턴츠 인코포레이티드 | 크실렌의 제조 방법 |
WO2016003611A1 (en) * | 2014-06-30 | 2016-01-07 | Exxonmobil Chemical Patents Inc. | Process for the production of para-xyxlene |
KR101920578B1 (ko) * | 2014-08-15 | 2018-11-20 | 엑손모빌 케미칼 패턴츠 인코포레이티드 | 방향족 화합물의 제조 방법 |
US9708233B2 (en) | 2014-08-15 | 2017-07-18 | Exxonmobil Chemical Patents Inc. | Aromatics production process |
US20170073285A1 (en) * | 2015-09-10 | 2017-03-16 | Uop Llc | Processes and apparatuses for toluene methylation in an aromatics complex |
US10059641B2 (en) * | 2015-09-25 | 2018-08-28 | Exxonmobil Chemical Patents Inc. | Conversion of non-aromatic hydrocarbon |
CN108430958B (zh) * | 2015-12-16 | 2021-01-01 | 环球油品公司 | 用于芳族化合物复合设备中的甲苯甲基化的方法及装置 |
WO2017105787A1 (en) | 2015-12-16 | 2017-06-22 | Uop Llc | Processes and apparatuses for olefin saturation in an aromatics complex |
WO2017187873A1 (ja) * | 2016-04-28 | 2017-11-02 | 旭化成株式会社 | 芳香族炭化水素含有化合物の製造方法 |
CN108250014A (zh) * | 2016-12-28 | 2018-07-06 | 中国石油天然气股份有限公司 | 一种异构化制备对二甲苯的方法 |
DE112018004207B4 (de) | 2017-08-15 | 2022-09-22 | Sabic Global Technologies B.V. | Schiefergas und Kondensat in Chemikalien |
US10793493B2 (en) | 2017-08-31 | 2020-10-06 | Uop Llc | Process for recovering benzene and fuel gas in an aromatics complex |
US10427993B2 (en) | 2017-08-31 | 2019-10-01 | Uop Llc | Process for recovering benzene and fuel gas in an aromatics complex |
US10392316B2 (en) * | 2017-10-11 | 2019-08-27 | Uop Llc | Process for minimizing benzene, toluene, and a recycle loop in a zero benzene aromatics complex |
US10308571B2 (en) * | 2017-10-11 | 2019-06-04 | Uop Llc | Process for minimizing benzene, toluene, and a recycle loop in a zero benzene aromatics complex |
KR20210024452A (ko) | 2018-06-25 | 2021-03-05 | 사빅 글로벌 테크놀러지스 비.브이. | 파라-크실렌 제조 방법 및 시스템 |
WO2020050092A1 (ja) * | 2018-09-03 | 2020-03-12 | Jxtgエネルギー株式会社 | キシレンの製造方法 |
EP3921296A1 (de) | 2019-02-04 | 2021-12-15 | China Petroleum & Chemical Corporation | Verfahren zur herstellung von phenol und xylolen |
US20200354293A1 (en) * | 2019-05-10 | 2020-11-12 | Uop Llc | Process and apparatus for dual feed para-xylene separation |
CN113527026A (zh) * | 2020-04-21 | 2021-10-22 | 国家能源投资集团有限责任公司 | 用于将轻质烷烃转化成芳香族化合物的系统和方法 |
KR102464480B1 (ko) | 2020-06-16 | 2022-11-07 | 주식회사 엘지화학 | 방향족 탄화수소의 제조방법 |
KR102464478B1 (ko) * | 2020-06-16 | 2022-11-07 | 주식회사 엘지화학 | 방향족 탄화수소 제조장치 |
CN114426879B (zh) * | 2020-10-15 | 2023-08-08 | 中国石油化工股份有限公司 | 含烃混合物的利用系统和方法 |
US11548842B1 (en) | 2022-06-01 | 2023-01-10 | Saudi Arabian Oil Company | Conversion of light naphtha to enhanced value aromatics in an integrated reactor process |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5609751A (en) * | 1994-07-26 | 1997-03-11 | Chevron Chemical Company | Para-xylene selective reforming/aromatization |
US6004452A (en) * | 1997-11-14 | 1999-12-21 | Chevron Chemical Company Llc | Process for converting hydrocarbon feed to high purity benzene and high purity paraxylene |
RU2184106C2 (ru) * | 1996-01-25 | 2002-06-27 | Эксон Кемикэл Пейтентс, Инк. | Способ получения параксилола |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4206035A (en) * | 1978-08-15 | 1980-06-03 | Phillips Petroleum Company | Process for producing high octane hydrocarbons |
JPH08301796A (ja) * | 1995-05-12 | 1996-11-19 | Koa Oil Co Ltd | 炭素数8の芳香族炭化水素の製造方法 |
US5685972A (en) * | 1995-07-14 | 1997-11-11 | Timken; Hye Kyung C. | Production of benzene, toluene, and xylene (BTX) from FCC naphtha |
US6565742B1 (en) * | 1997-09-03 | 2003-05-20 | Gtc Technology Inc. | Aromatics separation process and method of retrofitting existing equipment for same |
US20080287719A1 (en) * | 2004-12-30 | 2008-11-20 | Deng-Yang Jan | Process for para-xylene production from light aliphatics |
WO2008124228A1 (en) * | 2007-04-04 | 2008-10-16 | Exxonmobil Chemical Patents Inc. | Process and apparatus for para-xylene production |
EP2195107A1 (de) * | 2007-09-28 | 2010-06-16 | Basf Se | Verfahren zur gewinnung von aromatischen kohlenwasserstoffen aus einem kohlenwasserstoffgemisch |
JP2009242555A (ja) * | 2008-03-31 | 2009-10-22 | Mitsui Eng & Shipbuild Co Ltd | 廃プラスチックの処理方法及び処理装置 |
PL215253B1 (pl) * | 2008-06-26 | 2013-11-29 | Uop Llc | Sposób do wydzielania para-ksylenu z mieszaniny weglowodorów aromatycznych C8 i C9 i aparatura do wydzielania para-ksylenu z mieszaniny weglowodorów aromatycznych C8 i C9 |
JP4837114B2 (ja) * | 2010-03-26 | 2011-12-14 | 千代田化工建設株式会社 | 芳香族炭化水素の製造方法および芳香族炭化水素の製造プラント |
US8569559B2 (en) * | 2010-06-25 | 2013-10-29 | Exxonmobil Chemical Patents Inc. | Paraxylene production process and apparatus |
MY163515A (en) * | 2010-12-10 | 2017-09-15 | Exxonmobil Chemical Patents Inc | Method and apparatus for obtaining aromatics from diverse feedstock |
US8679321B2 (en) * | 2011-04-29 | 2014-03-25 | Uop Llc | Process for increasing benzene and toluene production |
JP5759262B2 (ja) * | 2011-05-24 | 2015-08-05 | Jx日鉱日石エネルギー株式会社 | キシレンの製造方法 |
-
2013
- 2013-03-14 MY MYPI2015701117A patent/MY183432A/en unknown
- 2013-03-14 JP JP2015536758A patent/JP6119062B2/ja active Active
- 2013-03-14 CA CA2888111A patent/CA2888111A1/en not_active Abandoned
- 2013-03-14 WO PCT/US2013/031146 patent/WO2014058465A1/en active Application Filing
- 2013-03-14 PL PL13845138T patent/PL2906663T3/pl unknown
- 2013-03-14 EP EP13845138.0A patent/EP2906663B1/de active Active
- 2013-03-14 MX MX2015004456A patent/MX2015004456A/es unknown
- 2013-03-14 US US13/830,189 patent/US10308567B2/en not_active Expired - Fee Related
- 2013-03-14 SG SG11201502727YA patent/SG11201502727YA/en unknown
- 2013-03-14 CN CN201380053326.4A patent/CN104919026B/zh active Active
- 2013-03-14 BR BR112015008035A patent/BR112015008035A2/pt not_active IP Right Cessation
- 2013-03-14 KR KR1020157012198A patent/KR101995233B1/ko active IP Right Grant
- 2013-03-14 IN IN3742DEN2015 patent/IN2015DN03742A/en unknown
- 2013-03-14 AU AU2013330434A patent/AU2013330434A1/en not_active Abandoned
- 2013-03-14 RU RU2015116113A patent/RU2664543C2/ru active
- 2013-09-25 TW TW102134542A patent/TWI622572B/zh active
- 2013-10-10 AR ARP130103691A patent/AR092980A1/es unknown
-
2015
- 2015-04-12 IL IL238173A patent/IL238173A0/en unknown
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5609751A (en) * | 1994-07-26 | 1997-03-11 | Chevron Chemical Company | Para-xylene selective reforming/aromatization |
RU2184106C2 (ru) * | 1996-01-25 | 2002-06-27 | Эксон Кемикэл Пейтентс, Инк. | Способ получения параксилола |
US6004452A (en) * | 1997-11-14 | 1999-12-21 | Chevron Chemical Company Llc | Process for converting hydrocarbon feed to high purity benzene and high purity paraxylene |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2787755C1 (ru) * | 2019-02-04 | 2023-01-12 | Чайна Петролеум Энд Кемикал Корпорейшн | Способ получения фенола и ксилолов |
Also Published As
Publication number | Publication date |
---|---|
IN2015DN03742A (de) | 2015-09-18 |
KR20150066586A (ko) | 2015-06-16 |
KR101995233B1 (ko) | 2019-07-02 |
MY183432A (en) | 2021-02-18 |
EP2906663B1 (de) | 2017-09-27 |
US10308567B2 (en) | 2019-06-04 |
SG11201502727YA (en) | 2015-05-28 |
TW201414698A (zh) | 2014-04-16 |
TWI622572B (zh) | 2018-05-01 |
WO2014058465A1 (en) | 2014-04-17 |
MX2015004456A (es) | 2015-07-14 |
CN104919026B (zh) | 2018-01-02 |
PL2906663T3 (pl) | 2018-03-30 |
EP2906663A4 (de) | 2016-06-08 |
JP6119062B2 (ja) | 2017-04-26 |
BR112015008035A2 (pt) | 2017-07-04 |
JP2015531405A (ja) | 2015-11-02 |
CN104919026A (zh) | 2015-09-16 |
US20140100398A1 (en) | 2014-04-10 |
RU2015116113A (ru) | 2016-11-27 |
EP2906663A1 (de) | 2015-08-19 |
AU2013330434A1 (en) | 2015-05-14 |
AR092980A1 (es) | 2015-05-13 |
CA2888111A1 (en) | 2014-04-17 |
IL238173A0 (en) | 2015-05-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2664543C2 (ru) | Способы и системы для получения ароматических соединений из углеводородов каталитического крекинга | |
JP5774122B2 (ja) | 多様な原料から芳香族化合物を得る方法及び装置 | |
US10508066B2 (en) | Methods and systems of upgrading heavy aromatics stream to petrochemical feedstock | |
TWI666194B (zh) | 用於芳香族複合設備中之芳香族甲基化之方法及裝置 | |
US10876054B2 (en) | Olefin and BTX production using aliphatic cracking reactor | |
TWI567058B (zh) | 使用選擇性吸附以分離二甲苯異構物之系統及方法 | |
CN108430958B (zh) | 用于芳族化合物复合设备中的甲苯甲基化的方法及装置 | |
EP3049381A1 (de) | Vorrichtung und verfahren zur isolierung von c8-aromaten | |
JP2017511829A (ja) | 高沸点炭化水素供給原料をより軽沸点の炭化水素生成物へ転換する方法 | |
TWI572588B (zh) | 用於形成具有經選擇量之c9芳族化物的c8芳族化物流的裝置及方法 | |
US11066344B2 (en) | Methods and systems of upgrading heavy aromatics stream to petrochemical feedstock | |
KR20160040599A (ko) | 방향족 콤플렉스에서 트랜스알킬화 원료 스트림을 제공하기 위한 스트림 분리 방법 및 시스템 | |
US20220033718A1 (en) | Aromatic recovery complex with a hydrodearylation step to process clay tower effluents | |
US9150467B2 (en) | Processes and apparatuses for preparing aromatic compounds | |
WO2020214872A1 (en) | Methods and systems of upgrading heavy aromatics stream to petrochemical feedstock |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PD4A | Correction of name of patent owner | ||
PC41 | Official registration of the transfer of exclusive right |
Effective date: 20210726 |